Plant hydrocarbon recovery process

Claim 2

A process using whole-plant biomass for production of fuel gases and organic liquids suitable for use as hydrocarbon fuels and as chemical feedstocks which comprises: (a) feeding a ground or chopped whole-plant biomass of a suitable particle size to an autothermic furnace containing a heating and drying zone, a thermal conversion zone and an oxidation zone wherein said furnace is a moving bed furnace and means are provided for exclusion of oxygen-containing gases from the inlet port, (b) heating and drying said biomass with reducing gases at a temperature within the range of from about 100° C. to 700° C., (c) removing said biomass from said heating and drying zone to said thermal conversion zone wherein a reducing atmosphere is present at a temperature of 200° C. to 1000° C., (d) exposing said biomass in thermal conversion zone to said temperature for a period of 1 second to 30 minutes, (e) removing said biomass from thermal conversion zone to oxidation zone wherein said biomass is partially oxidized to char at a temperature of 500° C. to 1000° C. in the presence of oxygen-containing gases selected from the group consisting of molecular oxygen and air, (f) removing said biomass from said oxidation zone wherein means are provided for exclusion of oxygen-containing gases from the outlet port, (g) removing product gases from heat and drying zone, (h) recovering liquid condensables from product gases.

Claim 3

The process of claim 1 wherein the ratio of said oxygen-containing gases to said biomass oxidized to char is within the range of from about 0.1 to about 2 pounds of oxygen as molecular oxygen per pound of char oxidized.

Claim 4

The process of claim 2 wherein said oxygen-containing gas is molecular oxygen.

Claim 5

The process of claim 1 wherein said autothermic furnace is a gravity autothermic furnace.

Claim 6

The process of claim 1 wherein said autothermic furnace is a rotating bed autothermic furnace.

Claim 7

The process of claim 1 wherein the said biomass comprises hydrocarbon-containing plants selected from the group of plant families consisting of Euphorbiaceae, Asclepiadaceae, Cactaceae, Apocynaceae, Pinaceae and Compositae families.

Claim 8

The process of claim 1 wherein said hydrocarbon-containing plants are selected from the group consisting of Euphorbia heterophylla, Euphorbia lathyrus, Euphorbia marginata, Asclepias syriaca, Calotropis procera and Apocynum sibiricum.

Claim 9

A process for production of fuel gases and organic liquids suitable for use as hydrocarbon fuels and as chemical feedstocks from hydrocarbon-containing biomass which process comprises: (a) grinding or chopping hydrocarbon-containing biomass to a particle size suitable for solvent extraction, (b) percolating said particles in a solvent suitable for hydrocarbon extraction to form a solvent extract of said hydrocarbon-containing biomass, (c) evaporating solvent from said solvent extract to obtain hydrocarbon resin extract, (d) feeding said hydrocarbon resin extract chopped or ground to a suitable particle size to an autothermic furnace containing a heating zone, a thermal conversion zone and an oxidation zone wherein means are provided for exclusion of oxygen-containing gases from inlet port, (d) heating said hydrocarbon resin extract with reducing gases at a temperature within the range from about 100° C. to 700° C., (e) removing said hydrocarbon resin extract from said heating zone to said thermal conversion zone wherein a reducing atmosphere is present at a temperature from about 200° C. to 1000° C., (f) exposing said hydrocarbon resin extract in said thermal conversion zone to said temperature for a period of from about 1 second to 30 minutes, (g) removing said hydrocarbon resin extract from said thermal conversion zone to said oxidation zone wherein said hydrocarbon resin extract is partially oxidized to char at a temperature of from about 50° C. to about 1000° C. in presence of oxygen-containing gases selected from the group consisting of molecular oxygen and air, (h) removing ash and char from said hydrocarbon resin extract from said oxidation zone wherein means are provided for exclusion of oxygen-containing gases from the outlet port, (f) removing product gases from heating zone, (j) recovering liquid condensables from product gases.

Claim 10

A process for production of fuel gases and organic liquids suitable for use as hydrocarbon fuels and as chemical feedstocks from hydrocarbon-containing biomass which process comprises: (a) grinding or chopping hydrocarbon-containing biomass to a particle size suitable for solvent extraction, (b) percolating said particles in a solvent suitable for hydrocarbon extraction to form a solvent extract of said hydrocarbon-containing biomass, (c) evaporating solvent from said solvent extract to obtain hydrocarbon resin extract, (d) feeding said hydrocarbon resin extract chopped or ground to a suitable particle size to an autothermic furnace containing a heating zone, a thermal conversion zone and an oxidation zone wherein means are provided for exclusion of oxygen-containing gases from inlet port, (d) heating said hydrocarbon resin extract with reducing gases at a temperature within the range from about 100° C. to 700° C., (e) removing said hydrocarbon resin extract from said heating zone to said thermal conversion zone wherein a reducing atmosphere is present at a temperature from about 200° C. to 1000° C., (f) exposing said hydrocarbon resin extract in said thermal conversion zone to said temperature for a period of from about 1 second to 30 minutes, (g) removing said hydrocarbon resin extract from said thermal conversion zone to said oxidation zone wherein said hydrocarbon resin extract is partially oxidized to char at a temperature of from about 50° C. to about 1000° C. in presence of oxygen-containing gases selected from the group consisting of molecular oxygen and air, (h) removing ash and char from said hydrocarbon resin extract from said oxidation zone wherein means are provided for exclusion of oxygen-containing gases from the outlet port, (f) removing product gases from heating zone, (j) recovering liquid condensables from product gases.

Claim 11

The process of claim 8 wherein the ratio of said oxygen-containing gases to said hydrocarbon resin extract oxidized to char in said oxidation zone is within the range of from about 0.1 to about 2 pounds of oxygen as molecular oxygen per pound of hydrocarbon resin extract oxidized.

Claim 12

The process of claim 9 wherein said oxygen-containing gas is molecular oxygen.

Claim 13

The process of claim 8 wherein said autothermic furnace is a gravity autothermic furnace.

Claim 14

The process of claim 8 wherein said autothermic furnace is a rotating bed autothermic furnace.

Claim 15

The process of claim 8 wherein said hydrocarbon-containing biomass comprises hydrocarbon-containing plants selected from the group of plant families consisting of Euphorbiaceae, Asclepiadaceae, Cactaceae, Apocynaceae, Pinaceae, and Compositae families.

Claim 16

The process of claim 13 wherein said hydrocarbon-containing plants are selected from the group consisting of Euphorbia heterophylla, Euphorbia lathyrus, Euphorbia marginata, Asclepias syriaca, Calotropis procera, Apocynum sibiricum, Grindelia squarrosa, Euphorbia tirucalli, and Asclepias tuberosa.